Oxidative and reductive leaching methods

Patent metadata

Field	Value
Publication number	US-2025034676-A1
Application number	US-202218717133-A
Country	US
Kind code	A1
Filing date	Dec 6, 2022
Priority date	Dec 7, 2021
Publication date	Jan 30, 2025
Grant date	—

Abstract

Disclosed herein are methods for leaching a material comprising one or more metals in a zero oxidation state and one or more chosen from metal oxides, metal hydroxides, and combinations thereof, wherein the method comprises contacting the material with an oxidizing acidic aqueous solution having a pH less than 6, and subsequently reducing the one or more chosen from metal oxides, metal hydroxides, and combinations thereof with a reducing agent. Also disclosed are methods comprising leaching a material to obtain an aqueous solution comprising metal ions, and separating the metal ions to obtain at least one essentially pure metal ion solution and/or at least one essentially pure solid metal ion salt. Further disclosed are methods comprising mechanically comminuting a material to obtain a black mass, and leaching the black mass.

First claim

1 . A method for leaching a material comprising one or more metals in a zero oxidation state and one or more chosen from metal oxides, metal hydroxides, and combinations thereof, wherein the method comprises:
contacting the material at a temperature ranging from 20° C. to 110° C. for a duration ranging from 10 minutes to 10 hours with an oxidizing acidic aqueous solution having a pH less than 6 and comprising one or more acids chosen from HCl, H 2 SO 4 , CH 3 SO 3 H, HNO 3 , and combinations thereof, and further comprising one or more chosen from O 2 , N 2 O, and combinations thereof, and subsequently reducing the one or more chosen from metal oxides, metal hydroxides, and combinations thereof at a temperature ranging from 20° C. to 100° C. for a duration ranging from 10 minutes to 10 hours with a reducing agent chosen from SO 2 , metabisulfite salts, bisulfite salts, thiosulfate salts, dithionate salts, H 2 O 2 , H 2 , and combinations thereof.

2 . The method according to claim 1 , wherein the oxidizing acidic aqueous solution comprises H 2 SO 4 and further comprises O 2 , N 2 O, or combinations thereof.

3 . The method according to claim 1 , wherein the reducing agent is SO 2 , and SO 2 is sparged through the solution at a rate of up to 20% of the total volume of the solution per minute.

4 . The method according to claim 1 , wherein the material is a lithium ion battery material comprising one or more chosen from black mass, cathode active material, cathodes, cathode active material precursors, and combinations thereof, and/or wherein the material comprises one or more chosen from nickel, cobalt, manganese, and combinations thereof.

5 . The method according to claim 1 , wherein the one or more metals in a zero oxidation state is chosen from nickel, cobalt, copper, aluminum, iron, manganese, rare earth metals, and combinations thereof, and/or wherein the metal oxides are chosen from nickel oxides, cobalt oxides, copper oxides, aluminum oxide, iron oxides, manganese oxides, rare earth oxides, and combinations thereof, and/or wherein the metal hydroxides are chosen from nickel hydroxides, cobalt hydroxides, copper hydroxides, aluminum hydroxide, iron hydroxides, manganese hydroxides, rare earth hydroxides, and combinations thereof.

6 . The method according to claim 1 , wherein the material comprises:
from 0.1 weight percent to 10 weight percent lithium, from 0 weight percent to 60 weight percent nickel, from 0 weight percent to 20 weight percent cobalt, from 0 weight percent to 20 weight percent copper, from 0 weight percent to 20 weight percent aluminum, from 0 weight percent to 20 weight percent iron, and from 0 weight percent to 20 weight percent manganese; wherein each weight percent is by total weight of the material, with the proviso that the content of at least one of nickel, cobalt, and manganese is more than 0 weight percent.

7 . The method according to claim 1 , wherein the material, or a precursor thereof, is pyrolyzed prior to leaching.

8 . The method according to claim 1 , wherein the oxidizing acidic aqueous solution comprises O 2 , the O 2 being provided as air, and the air being sparged through the solution at a rate corresponding to up to 20% of the total volume of the solution of O 2 being sparged through the solution per minute.

9 . The method according to claim 1 , further comprising adding an additional metal oxide and/or metal hydroxide after the contacting step and before the reducing step, and/or wherein contacting the material with an oxidizing acidic aqueous solution having a pH less than 6 causes a formation of hydrogen gas, and wherein after the formation of hydrogen gas, adding an oxidizing agent chosen from O 2 , N 2 O, and combinations, and/or wherein the oxidizing acidic aqueous solution has a concentration of acid ranging from 18 mol/L to 0.0001 mol/L.

10 . The method according to claim 1 , wherein, subsequent to the contacting step, the method further comprises adding an additional material comprising one or more chosen from metal oxides, metal hydroxides, metal carbonates, metal bicarbonate and combinations thereof.

11 . A method comprising:
leaching a material according to claim 1 to obtain an aqueous solution comprising metal ions, and separating the metal ions to obtain at least one essentially pure metal ion solution and/or at least one essentially pure solid metal ion salt.

12 . A method comprising:
mechanically comminuting at least one material chosen from a lithium ion battery, lithium ion battery waste, lithium ion battery production scrap, lithium ion cell production scrap, lithium ion cathode active material, and combinations thereof to obtain a black mass, and subjecting the black mass to the method according to claim 1 , optionally further comprising subjecting the at least one material to a heat treatment step.

13 . The method according to claim 1 , wherein, subsequent to the contacting step, the method further comprises adding a base, preferably wherein the base is chosen from CaO, a hydroxide salt, a carbonate salt, and combinations thereof, optionally wherein the hydroxide salt is chosen from LiOH, NaOH, KOH, NH 4 OH, Ca(OH) 2 , Ni(OH) 2 , Co(OH) 2 , Mn(OH) 2 and combinations thereof.

14 . The method according to claim 1 , wherein the oxidizing acidic aqueous solution further comprises hydrogen peroxide, provided that the one or more chosen from metal oxides or metal hydroxides comprising nickel cobalt or manganese contain these metals in an oxidation state of +2.

15 . The method according to claim 10 , wherein the additional material comprises nickel and/or cobalt, optionally wherein the additional material comprises cathode active material.

Assignees

• Basf Se

Inventors

• Smith Vincent
• Gerlach Till
• Muller Bernard
• Rohde Wolfgang
• Born Nils-Olof Joachim
• Schierle-Arndt Kerstin
• Jablonka Mark
• Syrma Alex

Classifications

• C22B23/043

  Sulfurated acids or salts thereof · CPC title

• C22B15/0071

  containing sulfur · CPC title

• C22B15/0067 Primary

  with acids or salts thereof · CPC title

• H01M10/54

  Reclaiming serviceable parts of waste accumulators · CPC title

• C22B47/00

  Obtaining manganese · CPC title